METHOD OF FLUE GAS PURIFICATION AND FLUE GAS PURIFIER

Abstract: A method for purifying flue-gases deriving from a combustion plant involves first drawing flue-gases from the plant and through a liquid volume by suction and then pressing the gases through a liquid, whereafter the purified flue-gases are discharged to the surroundings. During their passage through the liquid, the flue-gases are divided into the smallest possible flow units so as to achieve the best contact with the liquid. The method is carried out with the aid of a flue-gas purifier (5) which includes a liquid container (6), preferably a water container, which is divided into chambers (18-24). One set of chambers (18-21) forms a suction department (A) and another set of chambers (22-24) forms a pressure department (B). Walls (12, 14, 16) which form partitions between the chambers force the flue-gases to pass alternately through liquid and above the surface of the liquid. A pump (26) sucks the flue-gases through the suction department (A) and presses these gases through the pressure department (B). The walls (12, 14, 16) are provided at least partially with slots through which the flue-gases are forced to pass, therewith dividing the flue-gases into several flows, and the pump outlet (28) opens into a nozzle which finely divides the gaz and which is submerged in the liquid. As seen in the direction followed by the flue-gases, the first chamber (18) in the suction department (A) is provided with an inlet (25) for flue-gases arriving from the combustion plant, while the last chamber in the pressure department (B) is provided with an outlet (29) for the purified flue-gases.

Description: METHOD OF FLUE GAS PURIFICATION AND FLUE GAS PURIFIER The present invention relates to a gas purifier, and more particularly, but not exclusively, to the cleansing or purifying of flue-gases with the aid of a flue-gas purifier, whereby the efficiency of the combustion system is improved and the use of a conventional smoke stack is rendered unneces¬ sary. In the case of conventional combustion systems, it is not possible to recover all of the energy that can be recovered theoretically. This is because the flue-gases that leave the boiler must have a lowest temperature of about 250°C, in order to be able to rise up through the smoke stack and up into the air to a height at which the flue-gases and the contaminants carried thereby will be spread over an area which is suffi¬ ciently wide to prevent the occurrence of serious damage. Irrespective of the type of conventional flue-gas purifier used at present, it is necessary for the flue-gases to flow through the smoke stack at a given lowest velocity, which presumes a high gas temperature. This can present problems regarding the recovery of heat from the flue-gases when the temperature of the flue-gases exiting from the boiler to the smoke stack is lowered to an extent which influences the velocity of the outgoing gases. Consequently, when the fuel is combusted at a temperature of l,000 β C in the furnace itself, the flue-gas temperature in the boiler, in which heating is effected by the heat-carrying medium of the system, normally water, is normally lowered by 750 β C. The flue-gases exiting from the boiler will then have a temperature of 250 β C. The object of the present invention is to overcome the aforesaid problems. This object is achieved with a method and a flue-gas purifier according to the following Claims, which also disclose the individual characteristic features of the invention. The invention will now be described in more detail with reference to the accompanying drawings, in which Fig. 1 illustrates schematically and from above a heating system equipped with an inventive flue-gas purifier; Fig. 2 is a schematic longitudinal section view of an inven¬ tive flue-gas purifier; Fig. 3 is a schematic longitudinal section view of the flue- gas purifier shown in Fig. 2; and Fig. 4 is a schematic cross-sectional view of the flue-gas purifier shown in Figs. 2 and 3. Fig. 1 illustrates a heating plant 1 which includes an inventive flue-gas purifier. The plant 1 is housed in a container 2 and includes a combustion furnace 3, a boiler 4 in which heat exchange with the heat-carrying medium takes place, and an inventive flue-gas purifier 5. Fuel for combus¬ tion, for instance wood chips or oil, is taken from a fuel store 6 located outside the container 2, and charged to the furnace 3. The described arrangement in which the invention is applied with a plant or system in which the major part thereof is housed in a container has no significance with regard to the invention, since the invention can be applied with practically any type of combustion plant. According to the invention, the heat exchange effected in the boiler 4 is adapted so that the temperature of the flue-gases leaving the boiler will be maintained at about 100°C. Normal¬ ly, this temperature is not sufficient to discharge the flue- gases as effectively as is necessary. However, a temperature of 100°C is clearly sufficient to prevent damage to the boiler 4 and also to the flue-gas conduits leading from the boiler to the flue-gas purifier 5. According to a preferred embodiment, the inventive flue-gas purifier 5 includes a box-like container 6 which is made of welded steel sheet for instance, and has a rectangular shape when seen from above. The container bottom 7 has a V-shaped cross-section and accomadates an outfeed screw (not shown) in the apex 8 thereof. A partition wall 9 extends downwardly from the lid or cover 10 of the container 6 along the length of the container from end-wall to end-wall in a direction towards the container bottom 7, where it terminates at a distance of roughly one-third of the vertical distance from the apex 8 of the V-shaped bottom 7. This partition wall 9 may be insulated. The container 6 is filled partially with water to a level 11, which lies roughly at two-thirds of the container height above the apex 8 of the bottom 7. Although not shown, level sensors and water-filling and water-draining devices may be provided for the purpose of maintaining a desired volume of water in the container 6. A wall or baffle 12 extends transversely across the container 6 from a location approximately midway of the length of the container. This wall 12 defines a gap 13 between its upper edge and the container cover 10 and extends downwardly to terminate at a short distance beneath the water surface 11. Another wall or baffle 14 extends transversely across the container 6, between the wall 12 and the end-wall of the container 6, this end-wall including a flue-gas inlet 25. The wall 14 is attached to the container cover 10 and extends down towards the water level 11, but terminates short of the water level so as to form a gap 15. A further wall or baffle 16 is provided between the partition wall 9 and one long wall 17 of the container 6. The walls 12, 14 and 16 form a series of chambers 18-24 above the water level 11. The bottom end-edges of the walls 12, 14, 16 will preferably be slotted so as to have a comb-like configuration which functions to divide the flue-gases into many smaller flows, so that the flue-gases which pass through the chambers 18-24 and partially through the water will be divided into the smallest possible flow units for the best possible contact with the water. The partition wall 9 divides the container 6 into two longitu¬ dinally extending parts or compartments A and B above the water level 11. The one part A includes sequentially the chambers 18-21, wherein the flue-gas inlet 25 which receives flue-gases from the boiler 4 discharges into the chamber 18. The chambers 18-21 forming the part A thus lie sequentially between one long side 17 of the container 6 and the partition wall 9. The inlet 27 of an air pump 26, for instance a fan, is connected to the chamber 21 and located in the container cover 10, while the fan outlet 28 is located in the chamber 22 which lies opposite the chambers 20 and 21 but between the partition wall and the opposite container long wall. The chamber 24 lies opposite the chamber 18 between the partition wall 9 and the opposing long wall, while the chamber 23 lies between these chambers 22 and 24 centrally opposite the chamber 19. The chambers 22, 23 and 24 thus form the part B of the container 6. The fan outlet 28 opens out beneath the water level 11, suitably into a spray nozzle (not shown), which functions to spread the flue-gases throughout the water. An outlet 29 for purified and cooled gases is provided in the chamber 24, which is the last chamber in the series. The fan 26 is controlled by the pressure in the boiler 4 and in the part A of the container 6 by means of electronic control equipment not shown. In order to achieve proper combustion, there is preferably maintained in the boiler 4 a subpressure of about 5 millimeters water column, which can normally be achieved by causing the fan 26 to maintain a subpressure of about 10 millimeters water column in part A of the container 6. Naturally, different factors influence the pressure primarily in the boiler 4, although the fan 26 can be controlled readily to maintain the boiler pressure at a desired level with the aid of proper control equipment, wherein the pressure in the container part A will be held at an acceptable level in response to this control. It is essential that the pressure in the boiler 4 is correct for the combustion process, whereas the pressure in the container part A is less essential but will constantly lie somewhat beneath the boiler pressure, since the fan 26 primarily evacuates the container part A and secondarily the boiler 4. When the heating plant is in operation, the flue-gases flowing or sucked from the boiler 4 into the chamber 18 of the flue- gas purifier 5 have a temperature of about 100°C. As indicated by the arrow, the flue-gases continue from the chamber 18 through the gap 15 between the wall 14 and the water surface 11 and are divided into part-flows by virtue of the comb-like lower part of the wall 14, and impinge also on the water surface. The flue-gases swirl around in the chamber 19 and continue in the direction of the arrow through the gap 13 defined between the container cover 10 and the upper edge of the wall 12 into the chamber 20, in which the flue-gases continue to swirl and from which the gases pass out through the gap between the water surface 11 and the wall 16 and into the chamber 21, as indicated by the arrow. Naturally, the flue-gases will impinge on the surface of the water 11 during the whole of their transportation through the chambers in the container part A. The flue-gases are sucked from the chamber 21 into the fan 26 through the inlet 27, and then pass out from the fan through the outlet 28 and into the chamber 22 in part B of the container 6. Although not shown, the outlet 28 opens into a nozzle which is lowered into the water to a level between the bottom edge of the partition wall 9 and the water surface 11. The flue-gases are then urged through the chambers 23 and 24 in similar routes or while moving in similar patterns as the flue-gases in the chambers in the container part A, and finally reach the outlet 29 through which they are discharged to atmosphere. During their movement through the container 6, the flue-gases are divided into small bubbles, the more the better, which come into contact with the water in the container 6. The flue- gases are therewith cooled and particles of soot and other contaminants carried by the gases will precipitate into the water. In round numbers, the flue-gases contain 40% steam, 15% carbon dioxide and 35% nitrogen gas when entering the contain¬ er 6. After having passes through the container, the gases will contain between 6 and 15% carbon dioxide, this value varying in dependence on the pH of the water, and 35% nitro- gen. The steam is condensed in the container 6, due to the fact that container water is kept at a temperature beneath 100°C, the nitrogen gas is inert and natural and can therefore be discharged to atmosphere to no detriment, while the carbon dioxide emission lies within fully acceptable values. With the intention of maintaining the temperature of the water in the container 6 at the lowest possible level, preferably not above 37°C, the container may include a heat exchanger which functions to cool the water and also to enable further heat to be recovered in addition to that covered by the boiler 4. The container water will preferably be maintained at a pH above 7, in order to bind heavy metals in the flue-gases. This may be achieved with the aid of a device (not shown) which functions to deliver lime to the water, wherein the volumes in which the lime is dispensed may be controlled by a conven¬ tional detector or sensor means which monitors the pH of the water with respect to a preset pH value. The contaminants precipitated into the water sink to the bottom of the container and are removed therefrom when necessary by means of the earlier mentioned screw feed arrangement (not shown) . The invention is based on the concept of causing the flue- gases to pass through a container which has two departments A and B which are mutually separated with regard to the subpressures and overpressures in the routes followed by the flue-gases through the container 6, but which are mutually joined with regard to the water volume in the container 6, and by drawing flue-gases by suction into one department or part A and transferring the flue-gases from this container part into the second container part or department B under pressure. In addition, the flue-gases are finely divided as they pass through the comb-like bottom edges of the walls 12, 14, 16 and are released into the container part or department B through a spray nozzle. However, with regard to the purely constructive design of the inventive flue-gas purifier 5 it has been found that an unexpected positive effect is obtained by virtue of the fact that the water level in the subpressure container part A strives to increase while the water level in the overpressure container part B strives to decrease. However, instead of a constant level difference between the two container parts or departments, it has been found that a pumping effect is generated by virtue of a relatively regular raising and lowering of the water levels. This results, in turn, in greater turbulence and in more finely dividing of the flue- gases and in a varying resistance to the flue-gases as they pass into the gaps between the walls and the water surface 11. As a result of this "splashing effect", the contact surfaces between water and flue-gases is much greater than when the gases pass through stationary water. This effect improves both the cooling effect and the purifying effect. It will be understood that the described and illustrated embodiment of the flue-gas purifier is only one of several possible embodiments. For instance, the container parts A and B may well be arranged in some other sequence, for instance one after the other, in a circle, etc. , and that the container parts may include more or fewer chambers without departing from the inventive concept as defined in the following Claims.

Claims: CLAIMS 1. A method for purifying flue-gases deriving from a combustion plant, characterized by first drawing the flue- gases through a liquid volume by suction while dividing the flue-gases into smaller units, and then pressing the flue- gases through a liquid volume prior to discharging the flue- gases to the surroundings. 2. A method according to Claim 1, characterized by passing the flue-gases through a number of chambers during both the suction phase and the pressure phase, and therewith alternat¬ ing flue-gas flows outside and through said liquid volume. 3. A method according to Claim 1 or 2, characterized by transporting the flue-gases from the combustion plant and through the purifying process with the aid of a pump, for instance a fan, which is controlled to maintain a predeter¬ mined subpressure in the combustion plant. 4. A method according to any one of Claims 1-3, character¬ ized by lowering the temperature of the flue-gases to about 100°C prior to said gases reaching said liquid volume. 5. A method according to any one of the preceding Claims, characterized by adding an agent to the liquid volume so as to maintain the liquid volume at a pH value above 7. 6. A flue-gas purifier (5) for cleansing flue-gases deriving from a combustion plant (3, 4), comprising a closed liquid container (6), characterized in that the purifier includes a partition wall (9) which extends from the container cover (10) downwardly towards the container bottom (7) ; in that the liquid extends up in the container to a level (11) above the bottom edge of the partition wall (9), thereby forming two mutually separate departments (A, B) ; and in that the purifier further includes a pump (26) which functions to place one department (A) under a subpressure and the other department (B) under an overpressure, wherein the subpressure department (A) receives flue-gases from the combustion plant (3, 4) through an inlet (25), and the pump (26) passes the combustion gases from the underpressure department (A) to the overpres¬ sure department (B) , this latter department being provided with an outlet (29) for purified flue-gases. 7. A flue-gas purifier according to Claim 6, characterized in that the departments (A, B) are divided into chambers (18- 24) which are mutually separated by walls (14, 12, 16) which extend alternately from the container cover (10) down towards the liquid level (11) and from a distance beneath the contain¬ er cover (10) down beneath the liquid level (11), wherein the flue-gases are forced to pass alternately through the liquid and through the chambers above the liquid level (11). 8. A flue-gas purifier according to Claim 7, characterized in that the bottom end of at least one of the walls (14, 12, 16) is slotted. 9. A flue-gas purifier according to any one of Claims 6-8, characterized in that the liquid is water. 10. A flue-gas purifier according to any one of Claims 6-9, characterized by a screw which functions to discharge from the container (6) contaminants that are precipitated from the flue-gases into the liquid. 11. A flue-gas purifier according to any one of Claims 6-10, characterized by means for delivering to the liquid an agent which will maintain the pH of the liquid at a value above 7 and for monitoring the pH of the liquid. 12. A flue-gas purifier according to any one of Claims 6-11, characterized in that the outlet from the pressure side of the pump (26) discharges into a spray nozzle located beneath the liquid level (11). 13. A heating plant which includes a fuel store (6), a furnace (3), a boiler (4) and a flue-gas purifier (5), characterized in that the furnace (3), the boiler (4) and the flue-gas purifier (5) are housed in a container (2).

Inventors: BOGG ANDERS, HEDBERG SOEREN, BOGG, ANDERS, HEDBERG, SOEREN
Applicants: BOGG ANDERS, HEDBERG SOEREN, MASARNA I MORA AB, BOGG, ANDERS, HEDBERG, SOEREN
Application year: 1994
Main classification: B01D53
IPC codes: B01D47, B01D53, F23J15